Method of producing viscose rayon



METHOD OF PRODUCING VISCOSE RAYON Wayne A. Sisson, Media, Pa., assignor to American Viscose Corporation, Philadelphia, Pa., a corporation of Delaware No-Drawing. Filed Nov. '3, 1954, Ser. No. 466,679

12 Claims. (Cl. 18-54) tion and after shredding the treated cellulose material, it.

is allowed to age. The aged alkali cellulose is then within certain composition limits which will be defined hereinafter. The most readily distinguishable characteristicsas compared to conventional filaments include a smooth, non-crenulated surface and the filaments consist entirely of skin. v

This invention contemplates the use of alkylene oxide adducts of urea and biuret having up to 100 or more of a compound in which each of the amino hydrogen converted to a xanthate by treatment with carbon disulfide. The cellulose xanthate is subsequently dissolved in a caustic soda solution in an amount calculated to provide a viscose of the desired cellulose and alkali content. After filtration, the viscose solution is allowed to ripen and is subsequently extruded through a shaped orifice into a suitable coagulating and regenerating bath.

In the productionof shaped bodies such asfilaments, the viscose solution is extruded through a spinneret into a coagulating and regenerating bath consisting of an aqueous'acid solution containing zinc sulfate. The filament may subsequently be passed through a hot aqueous bath where it is stretched to improve its properties such as tensile strength. The filament may then be passed through a dilute aqueous solution of sulfuric acid and sodium sulfate to complete the regeneration of the cellulose, in case it is'not completely regenerated upon leaving -the stretching stage. The filament is subsequently subjected to'washing, purification, bleaching, possibly othertreat ing operations and drying, being collected'either before or after'these treatments.

The filaments as formed by the conventional methods consist of a skin or outer shell portion and a core portion with a sharp line of demark'ationbetween-the two. The cross-section of the-filaments exhibits a very irregular or crenulated exteriorsurface when even small amounts of zinc salts or certain other polyvalent metal salts are present in the spinning bath. "The skin and core portions of the filament represent differences in structure and these "different portions possess difierent- -.swelling and staining-characteristics, the latter permitting 'a'ready identification ofskin and core. irregular and crenulated surface structure has a relatively low abrasion resistance and readily picks up foreign particlessuchas dirt. Although the core portion possesses a relatively "high tensile strength, it has a low abrasion .:resistance....and a low flex-life, is subject to fibrillation and is. relatively stilt. l

It has now been discovered that the presence of small shaped bodies-of regenerated cellulose such as filaments, films, sheets and the like composed of all skin and having improved properties and characteristics providing that the.

amount of the adduct is maintained within certain limits the composition of the spinning bath is maintained The sharply atoms has been replaced with an ethanol radical. It is not necessary, however, that all of the amino hydrogens be replaced nor is it necessary that the ethylene oxide chains replacing the different hydrogen atoms be the same in each instance. V

The term adduct is used herein to simplify the disclosure and description and designates a N-substituted urea or biuret formed by the reaction between an alkylene oxide and urea or biuret wherein the alkylene oxide .or the polyoxyalkylene chain replaces one or more of the hydrogen atoms attached to one or more of the nitrogen atoms.

These adducts are water-soluble compounds corresponding to the formulas and p (alkyleneo ide),.H

where R isI-l or (alkylene oxide) H, n is from 1 to about -and the total number of alkylene oxide units per molecule is between 1 and about 100.

'1 'he production of all skin products requires that certain minimum amounts of the alkylene oxide adduct be in solution in the viscose min the spinning bath. Therefore, the alkylene oxide adduct must have sufiicient solubility to permit the minimum amount of the adduct to be dissolved in the viscose or the spinning bath or both. The adduct may be conveniently added to the viscose in the form of a solution in alkali or water and to the spinning bath in a solution of water or of the spinning bath. Where the alkylene oxide adduct of urea is to be added to the viscose, the amount of the adduct which is incorporated in viscose must be at least about 0.25 by weight of the cellulose in the viscose and may vary up to about 4%, preferably, the amount varies from 0.5% to 2.5%. Lesser amounts do not result in the production of products consisting entirely of skin and greater amounts affect adversely the physical properties of the products. Amounts within the preferred range aremost effective in enhancing the characteristics and properties Patented Mar. l4, 1961 of the products. The adduct of urea may be added at any desired stage in the production of the viscose such as in the preparation of the refined wood pulp for the manufacture of viscose, before or during the shredding of the alkali cellulose, to the xanthated cellulose while it is being dissolved in the caustic solution or to the viscose solution before or after filtration. The adduct is preferably added after the cellulose xanthate has been dissolved in the caustic solution and prior to filtration.

The viscose may contain from about 6% to about 8% cellulose, the particular source of the cellulose being selected for the ultimate use of the regenerated cellulose product. The caustic soda content may be from about 4% to about 8% and the carbon disulfide content may be from about 30% to about 50% based upon the weight of the cellulose. The modified viscose, that is, a viscose containing the small amount of adduct, may have a salt test above about 7 and preferably above about 9 at the time of spinning or extrusion.

In order to obtain the improvements enumerated hereinbefore, it is essential that the composition of the spinning bath be maintained within a well defined range. The presence of the alkylene oxide adducts of urea in the viscose or in the spinning bath combined with these limited spinning baths results in the production of yarns of improved properties such as high tenacity, high abrasion resistance, high fatigue resistance and consisting of filaments composed entirely of skin.

Generically and in terms of the industrial art, the spinning bath is a low acid-high zinc spinning bath. The bath should contain from about 10% to about 25% sodium sulfate and from about 3% to about zinc sulfate, preferably from 15% to 22% sodium sulfate and from 4% to 9% zinc sulfate. Other metal sulfates such as iron, manganese, nickel and the like may be present and may replace some of the zinc sulfate. The temperature of the spinning bath may vary from about 25 C. to about 80 C., preferably between about 45 C. to about 70 C. In the production of the all skin type filaments, the temperature of the spinning bath is not critical, however, as is well known in the conventional practice in the art, certain of the physical properties such as tensile strength vary directly with the temperature of the spinning bath. Thus, in the production of filaments for tire cord purposes in accordance with the method of this invention, the spinning bath is preferably maintained at a temperature between about 55 C. and 65 C. so as to obtain the desired high tensile strength.

The acid content of the spinning bath is balanced against the composition of the viscose. The lower limit .of the acid concentration, as is Well known in the art,

is just above the slubbing point, that is, the concentra-. tion at which small slubs of uncoagulated viscose appear in the strand as it leaves the spinning bath. For commercial operations, the acid concentration of the spinning bath is generally maintained about 0.4% to 0.5% above the slubbing point. For any specific viscose composition, the acid concentration of the spinning bath must be maintained above the slubbing point and below the point at which the neutralization of the caustic of the viscose is sufficiently rapid to form a filament having a skin and core. There is a maximum acid concentration for any specific viscose composition beyond which the neutralization is sufficiently rapid to produce filaments having a skin and core. For example, in general, the acid concentration of the spinning baths which are satisfactory for the production of the all skin products from a 7% cellulose, 6% caustic-viscose and containing the adducts of urea lies between about 5% and about 7.8%. The acid concentration may be increased as the amount of adduct is increased and also as the salt test of the viscose is increased. There is an upper limit, however, for the acid concentration based upon the amount of additive and the concentration of caustic in the viscose. All skin products cannot be obtained if the acid concentration is increased above the maximum value although the amount like.

of the adduct of urea is increased beyond about 4% while other conditions are maintained constant. Increasing the caustic soda content of the viscose beyond about 8% is uneconomical for commercial production methods. For example, a viscose containing about 7% cellulose, about 6% caustic soda, about 41% carbon disulfide, 2% of an ethylene oxide adduct of urea containing about 20 ethylene oxide units per molecule and having a salt test of about 10 when extruded into spinning baths containing 16 to 20% sodium sulfate, 4 to 8% zinc sulfate and sulfuric acid not more than about 7.8%, results in the production of all skin filaments. Lesser amounts of sulfuric acid may be employed. Greater amounts of sulfuric acid result in the production of products having skin and core. A lowering of the amount of adduct of urea, the lowering of the caustic soda content or the lowering of the salt test of the viscose reduces the maximum permissible acid concentration for the production of all skin filaments. In any event, it has been determined that the maximum concentration of acid which is permissible for the production of all skin products is about 8%.

The presence of the adducts of urea in the viscose retards the coagulation and, therefore, the amount of adduct employed must be reduced at high spinning speeds. Thus, for optimum physical characteristics of an all skin yarn formed from a viscose as above and at a spinning speed of about 50 meters per minute, the adduct is employed in amounts within the lower portion of the range, for example, about 0.5%. The determination of the specific maximum and optimum concentration of acid for any specific viscose, spinning bath and spinning speed is a matter of simple experimentation for those skilled in the art. The extruded viscose must, of course, be immersed or maintained in the spinning bath for a period sufficient to effect relatively complete coagulation of the viscose, that is, the coagulation must be sumcient so that the filaments will not adhere to each other as they are brought together and withdrawn from the bath.

In the production of filaments for such purposes as the fabrication of tire cord, the filaments are preferably stretched after removal from the initial coagulating and regenerating bath. From the initial spinning bath, the filaments may be passed through a hot aqueous bath which may consist of hot water or a dilute acid solution and may be stretched from about 70% to about 120%, preferably between and Yarns for other textile purposes may be stretched as low as 20%. The precise amount of stretching will be dependent upon the desired tenacity and other properties and the specific type of product being produced. It is to be understood that the invention is not restricted to the production of filaments and yarns but it is also applicable to other shaped bodies such as sheets, films, tubes and the like. The filaments may then be passed through a final regenerating bath which may contain from about 1% to about 5% sulfuric acid and from about 1% to about 5% sodium sulfate with or without small amounts of zinc sulfate if regeneration has not previously been completed.

The treatment following the final regenerating bath, or the stretching operation where regeneration has been completed, may consist of a washing step, a desulfurizing step, the application of a finishing or plasticizing material and drying before or after collecting, or may include other desired and conventional steps such as bleaching and the The treatment after regeneration will be dictated by the specific type of shaped body and the proposed use thereof.

Regenerated cellulose filaments prepared from viscose containing the small amounts of the water-soluble alkylene oxide adducts of urea and spun in the spinning baths of limited acid content have a smooth or noncrenulated surface and consist substantially entirely of skin. Because of the uniformity of structure throughout the filament, the swelling and staining characteristics are uniform throughout the cross-section of the filament.

bath in place of adding the adduct to the viscose.

Filaments produced pursuant to this invention and con sisting entirely of skin have a high toughness and a greater flexing life than filaments are produced according to prior methods which may be attributed by the uniformity in skin structure throughout the filament. Although the twisting of conventional filaments, as in the production of tire cord, results in an appreciable loss of tensile strength, there is appreciablyjlejsslloss intensile strength in the production of twisted cords from the filaments consisting entirely of skin; ,Pfilaments prepared from viscose containing the adducts of urea have a high tensile strength as compared to normal regenerated cellulose filaments, have superior abrasion and fatigue resistance characteristics and. have a'high flex-life; Siich filaments are highly satisfactory for the production ofcords for the reinforcement of rubber products such as pneumatic tire casings, but the filaments are not restricted to such uses and may be used for other textile applications.

Like improvements in the characteristics and properties of the products are also obtained by incorporating the alkylene oxide adducts of urea or biuret in'the spinning It is essential that the composition of the spinning bath, particularly the acid concentration, be maintained within the limits set forth hereinbefore. In order to produce products-consisting of all skin, the amount of the alkylene oxide adduct of urea dissolved in the spinning bath must be at least about 0.05% by weight and is preferably maintained at about 0.1%. The upper limit does not appear to be critical as in the incorporation of the adducts in the viscose. The upper limit is dependent upon the solubility of the particular adduct and by economic considerations since amounts exceeding about 0.2% are not more effective in improving the properties of the products.

It is obvious that the adducts may be added to both the viscose and the spinning bath, if desired. In such instance, it is also essential to maintain the amounts of the adduct in the viscose and in the spinning bath, and the composition of the spinning bath within the stated limits. The all skin products of improved properties are obtained only when the spinning operation in the presence of the alkylene oxide adducts of urea or biuret 'is carried out withinthe spinning bath composition as set forth hereinbefore.

The invention may be illustrated by reference to the soda, and having a total carbon disulfide content of about 41%. The viscose solutions were prepared by xanthating alkali cellulose by the introduction of 36% .carbon disulfide based on the Weight of the cellulose and oxide adduct of urea was added to the solution and mixed for about /2 hour before allowing the viscose to ripen.

Example 1 Approximately 1% (based on the weight of the cellulose) of an ethylene oxide adduct of urea containing about 20 units of ethylene oxide per molecule of urea was added to and incorporated in the viscose as described above. The viscose employed in the spinning of filaments had a salt test of 10.4. The viscosewas extruded through a spinneret to form a 1650 denier, 720 filament cord at a rate of about 22 meters per minute. The coagulating and regenerating bath was maintained at a temperature of about 60 C. and contained 7.2% sulfuric acid, 8% zinc sulfate and 17% sodium sulfate. The cord was stretched about 90%, was hedfree of acids andsalts' by treatment with water at about 95 C. on thread advancing reels, dried and collected on cones; The individual filaments have a smooth, non-crenulated exterior surface and consist entirely of skin, no core being detectable at high magnification (e.g. 1500X). Thej filaments of a control yarn spun with the same viscose but without the addition of the modified agent and spun under the same conditions, exhibit a very irregular and serrated surface and are composed of about 75% skin and the balance core with a sharp line of demarkation between the skin and core. Other physical properties'ai'e set forth in the table'which follows the examples. 0

Example 2 containing 7.2% sulfuric acid, 8% zinc sulfate and 17% .45 preparation of regenerated cellulose filaments from a -voscose containing about 7% cellulose, about 6% caustic sodium sulfate. The bath was maintained at a temperature of 60 C. The extrusion rate was about 22 meters per minute. The cord was stretched about washed free of acids and salts by treatment with water at about C. on thread-advancing reels, dried and collected on cones.

The individual filaments were readily distinguishable from control filaments in that they have a smooth, noncrenulated surface and consist entirely of skin. Control filaments have a very irregular and serrated surface and consist of about 75% skin and the balance core with a sharp line of demarkation between the skin and core.

Other physical characteristics are set forth in the table Example 3 A viscose solution as described above (no adduct added) having a salt test of 9.7 was spun into a 210 denier, filament yarn by extrusion into a spinning bath containing 7.6% sulfuric acid, 7.9% zinc sulfate, 19% sodium sulfate and 0.1% of an ethylene oxide adduct of urea containing about 20 ethylene oxide units per molecule of urea. The bath was maintained at 60 C. and the extrusion rate was about 22 meters per minute. The filaments were passed through a hot water bath maintained at about 95 C. and stretched about 82%. The yarn was collected in a spinning box, washed free of acid and salts and dried. l

The filaments have a smooth, non-crenul-ated surface and consist entirely of skin while control filaments have a very irregular and serrated surface and consist of about 75% skin and-the balance core with a sharp line of demarkation between the skin and core. Other physical characteristics are set forth in the table which follows the examples.

Example 4 To a viscose as described above, there was added 2% of an ethylene oxide adduct of urea containing 4 ethylene oxide units per molecule of urea. The viscose had a salt test of 9.0 and was spun into a 210 denier, 120 filament yarn by extrusion into a spinning bath containing 7.6% sulfuric acid, 8% zinc sulfate, 19% sodium sulfate, and 0.1% of an ethylene oxide adduct of urea containing 20 ethylene oxide units per molecule. of urea. trusion rate was about 22 meters per minute. 'The filaments were subsequently passed through a hot water bath at 95 C. and stretched about 82%. The yarn was collected in a spinning box, washed free of acids and salts and dried. I

The bath was maintained at 60 C. and the'ex- The individual filaments were readily distinguishable from control filaments in that they have a smooth, noncrenulated surface and consist entirely of skin while the control filaments have a very irregular and serrated surface and consist of about 75% skin and the balance core with a sharp line of demarkation between the skin and the core. Other physical properties are set forth in the table which follows the examples.

Example To a viscose as described above, there was added 1% of an ethylene oxide adduct of urea containing 20 ethylene oxide units per molecule of urea. The viscose had a salt test of 11 and was spun into a 210 denier, 120 filament yarn by extrusion into a spinning bath containing 7.6% sulfuric acid, 8% zinc sulfate, 21% sodium sulfate, and 0.1% of an ethylene oxide adduct of urea containing 20 ethylene oxide units per molecule of urea. The bath was maintained at 60 C. and the extrusion rate was about 22 meters per minute. The filaments were subsequently passed through a hot,water bath at 95 C. and stretched about 82%. The yarn was collected in a spinning box, washed free of acids and salts and dried.

The individual filaments were readily distinguishable from control filaments in that they have a smooth, noncrenulated surface and consist entirely of skin while the control filaments have a very irregular and serrated surface and consist of about 75% skin and the balance core with a sharp line of demarkation between the skin and the core. Other physical properties are set forth in th table which follows the examples.

Example 6 To a viscose as described above, there was added 1% of an ethylene oxide adduct of urea containing 40 ethylene oxide units per molecule of urea. The viscose had a salt test of 10.7 and was spun into a 210 denier, 120 filament yarn by extrusion into a spinning bath containing 7.7% sulfuric acid, 8.6% zinc sulfate, 21% sodium sulfate, and 0.1% of an ethylene oxide adduct of urea containing 20 ethylene oxide units per molecule of urea. The bath was maintained at 60 C. and the extrusion rate was about 44 meters per minute. The filaments were subsequently passed through a hot water bath at 95 C. and stretched about 74%. The yarn was collected in a spinning box, washed free of acids and salts and dried.

The individual filaments were readily distinguishable from control filaments in that they have a smooth, noncrenulated surface and consist entirely of skin while the control filaments have a very irregular and serrated surface and consist of about 75% skin and the balance core with a sharp line of demarkation between the skin and the core. Other physical properties are set forth in the table which follows the examples.

Example 7 spinning box, washed free of acid and salts and dried.

The individual filaments have a very irregular and serrated surface and consist of about 75% skin and the balance core with a sharp line of demarkation between the skin and the core. Other characteristics are set forth in the table which follows.

Tenacity, Grams Elongation,

per denier Percent Skin,

Percent Wet Dry Wet Dry Example 1 3. 2 4. 3 31 11 100 Example 2..- 3. 2 4. 3 30 11 100 Example 3. 2. 6 3. 5 29 24 100 Example 4. 2. 5 3. 1 26 21 100 Example 5- 2. 5 8. 4 27 22 100 Example 6. 1. 3 2. 2 20 16 100 Example 7 (Con 2. 1 2. 8 27 21 75 It will be noted that the tenacity of the filaments of Example 6is low. This is occasioned by an extrusion rate double of that employed in the other examples. The tenacity may be increased somewhat by employing lower extrusion rates or by reducing to about 0.5% the amount of ethylene oxide adduct of urea added to the viscose.

Although the tenacity and elongation are the only properties set forth, they have been chosen because of the ease and simplicity with which such properties may be determined. In some instances, products made in accordance with this invention do not exhibit large or great improvements in tenacity and elongation (Example 4), however, the products consist of a smooth-surfaced, all skin structure and possess improved abrasion resistance, flex-life and other properties as disclosed hereinbefore.

One of the properties of viscose rayon which has limited its uses is its relatively high cross-sectional swelling when wet with water, this swelling amounting to from about 65% to about for rayon produced by conventional methods. Rayon filaments produced in accordance with the method of this invention have an appreciably lower cross-sectional swelling characteristic, the swelling amounting to from about 45% to about 60%.

The modifier of this invention may be added to any desired viscose such as those normally used in industry, the specific viscose composition set forth above, being merely for illustrative purposes. The alkylene oxide adduct of urea or biuret may be added at any desired stage in the production of the viscose and may be present in the cellulosic raw material although it may be necessary to adjust the amount present to produce a viscose having the proper proportions of the adduct at the time of spinning.

The term skin is employed to designate that portion of regenerated cellulose filaments which is permanently stained or dyed by the following procedure: A microtome section of one or more of the filaments mounted in a wax block is taken and mounted on a slide withv Meyers albumin fixative. After dewaxing in xylene, the section is placed in successive baths of 60% and 30% alcohol for a few moments each, and it is then stained in 2% aqueous solution of Victoria Blue BS cone. (General Dyestuifs Corp.) for l to 2 hours. At this point, the entire section is blue. By rinsing the section first in distilled water and then in one or more baths composed of 10% water and dioxane for a period varying from 5 to 30 minutes depending on the particular filament, the dye is entirely removed from the core, leaving it restricted to the skin areas.

While preferred embodiments of the invention have been disclosed, the description is intended to be illustrative and it is to be understood that changes and variations may be made without departing from the spirit and scope of the invention as defined by the appended claims.

I claim:

1. In a method of producing shaped bodies of regenerated cellulose consisting substantially entirely of skin, the step which comprises extruding viscose into an aqueous spinning bath in the presence of a substance selected from the group consisting of water-soluble compounds (alkylene oxide) H wherein R is selected from the group consistingof H and (alkylene oxide) H, n is from 1 to 100 and the total number of alkylene oxide units per molecule is between 1 and 100, thetbath containing from about to 25% sodium sulfate, from about 3% to zinc sulfate and sulfuric acid, the sulfuric acid content of the spinning bath exceeding the slubbing point but not exceedingtabout 8%, the substance being present in an amount of from about 0.25% to about 4%, based upon the weight of the cellulose in the viscose, when present in the viscose and of at least about 0.05%, based upon the weight of the spinning bath, when present in the spinning bath.

2. The step in the method as defined in claim 1 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula where R is selected from the group consisting of H and (C H O) H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and 50.

3. The step in the method as defined in claim 1 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula where R- is selected from the group consisting of H and (C H O),,H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and 50.

4. In a method of producing shaped bodies of regenerated cellulose consisting substantially entirely of skin the steps which comprise adding to and incorporating in a viscose from about 0.25% to about 4%, based upon the weight of the cellulose in the viscose, of a subtance selected from the group consisting of water-soluble compounds and mixtures of w tor-soluble compounds ponding to the formulas.

/(alkyle:ne oxide) rill and where R is selected from the group consisting of H and (alkylene oxide) H, n is from 1 to and the total number of alkylene oxide units per molecule is between 1 and 100, and extruding the viscose into an aqueous spinning bath containing from about 10% to 25% sodium sulfate, from about 3% to 15%- zinc sulfate and sulfuric acid, the sufuric acid content of the bath exceeding the slubbing point but not exceeding about 8%.

5. The steps in the method as defined in claim 4 where in the substance selected is a mixture of water-solubl compounds corresponding to the formula where R is seletced from the group consisting of H and (C H O) H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and 50.

6. The steps in the method as defined in claim 4 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula -where R is selected from the group consisting of H and (C H O) H, n is from 1 to 50 and the total number of (alkylene oxide) nH (alkylene oxide) in wherein R is selected from the group consisting of H and (alkylene oxide) H, n is from 1 to 100 and the total number of alkylene oxide units per molecule is between 1 and 100, and sulfuric acid, and extruding viscose into the spinning bath, the sulfuric acid content of the bath exceeding the slubbing point but not exceeding about 8%.

8. The method as defined in claim 7 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula (armour:

where R is selected from the group consisting of H and (C H O),,H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and 50.

9. The method as defined in claim 7 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula where R is selected from the group consisting of H and (C H 0),,H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and 50.

10. An aqueous spinning bath for the production of regenerated cellulose products consisting substantially entirely of skin from viscose containing from about 10% to 25% sodium sulfate, from about 3% to zinc sulfate, from about 5% to about 8% sulfuric acid and at least 0.05% of a substance selected from the group consisting of water-soluble compounds and mixtures of watersoluble compounds corresponding to the formulas (alkylene oxide) H wherein R is selected from the group consisting of H and (alkylene oxide) H, n is from 1 to and the total number of alkylene oxide units per molecule is between 1 and 100.

11. An aqueous spinning bath as defined in claim 10 wherein the substance selected is a mixture of water-soluble compounds corresponding to the formula where R is selected from the group consisting of H and (C H O),,H, n is from 1 to 50 and the total number of ethylene oxide units is between 4 and S0.

References Cited in the file of this patent UNITED STATES PATENTS 2,125,031 Polak July 26, 1938 2,312,152 Davis Feb. 23, 1943 2,373,712 Schlosser Apr. 17, 1945 2,593,466 MacLaurin Apr. 22, 1952 

1. IN A METHOD OD PRODUCING SHAPED BODIES OF REGENERATED CELLULOSE CONSISTING SUBSTANTIALLY ENTIRELY OF SKIN, THE STEP WITH COPMPRISES EXTRUDING VISCOSE INTO AN AQUEOUS SPINNING BATH IN THE PRESENCE OF A SUBSTANCE SELECTED FROM THE GROUP CONSISTING OF WATER-SOLUBLE COMPOUNDS AND MIXTURES OF WATER-SOLUBLE COMPOUNDS CORRESPONDING TO THE FORMULAS 